Deformable, rigid polystyrene foam board

ABSTRACT

Provided are methods for producing a high strength, but easily deformed, polystyrene foam board that can endure repeatedly deformations from its original configuration into more complex curved shapes without damaging the board integrity or substantially reducing its structural strength. Also provided are rigid polystyrene foam boards produced by this method that exhibit improved bending and impact resistance while substantially retaining or improving other properties, for example, the thermal dimensional stability and fire resistance, exhibited by corresponding conventional XPS foam boards. The foamable compositions may incorporate one or more of a variety of polymer processing aids for the purpose of altering the performance of the final foam products, thereby allowing the properties of the final foam product to be customized to some degree.

TECHNICAL FIELD AND INDUSTRIAL APPLICABILITY

The present invention relates to compositions and methods for producinghigh strength-easy deformation (HS-ED) rigid extruded polystyrene (XPS)foam board suitable for insulation applications, particularly forexterior insulation finish system (EIFS) for building construction,highway insulation structures having a non-planar surfaces andstructural foam products. The rigid polystyrene foam board producedaccording to the invention may also exhibit improved impact resistancerelative to corresponding foam board products produced usingconventional compositions and methods and may, therefore, be suitablefor structural foam products as well. The present invention may also beapplied to both conventional cellular foams (i.e., typically exhibitingcell densities of around 10⁴-10⁶ cells/cm³), microcellular foams (i.e.,those typically having cell densities of around 10⁷-10⁹ cells/cm³) andpossibly ultramicrocellular foams (i.e., those typically having celldensities of around 10⁹-10¹² cells/cm³). As the average cell sizedecreases for a given material, the expansion factor also decreases andthe polymer strength tends to be increased for maintaining cellintegrity, by at least in part reducing cell coalescence and maintainingrelatively thicker cell walls.

BACKGROUND OF THE INVENTION

This invention relates to foam insulating products, particularlyextruded polystyrene foam, containing a minor amount of one or moreadditives including, for example, one or more vinyl resins, sufficientto achieve a desired combination of flexibility and strength. The rigidextruded polystyrene foam boards manufactured according to the inventioncan be deformed repeatedly at room temperature in the process ofcreating shaped board forms having one or more curvatures, bends ordeformations, without resiling, cracking or breaking, whilesubstantially retaining the thermal and physical properties of theoriginal, non-deformed board.

As will be appreciated, the ability to deform expanded foam insulationboards into various shapes to fit within the architectural design of astructure while tending to preserve its structural and insulatingintegrity is particularly advantageous for construction applications.This ability is also desirable for expanded foam insulation boardsintended for use as exterior wall insulation board or as highwayunderground insulation board for concrete structures having waved,curved, oscillating or other rounded complex profiles.

SUMMARY OF THE INVENTION

The present invention relates to producing a high strength-easydeformation (HS-ED) rigid polystyrene foam board that can be repeatedlydeformed from its original substantially planar configuration into acurved shape without resiling, cracking or otherwise damaging the boardintegrity or substantially reducing the structural strength of theboard, even after repeated deformations. The present invention producesrigid polystyrene foam boards that exhibit improved bending and impactresistance, thereby improving the performance and handling of thin rigidXPS foam board, while substantially retaining or improving otherproperties, for example, the thermal dimensional stability and fireresistance, exhibited by corresponding conventional XPS foam boards.

A variety of polymer processing aids (PPA) may be included in thepolymer melt in order to alter the processing performance of the polymermelt including, for example, reducing melt fractures, improving surfaceproperties in a variety of polyolefin articles; improving stability,reducing shear, increasing output with similar or reduced force,improving temperature control of the melt and reducing melt friction.Similarly, the composition of the base polymer can be altered throughthe addition of one or more other polymers and copolymers to the melt toform a blended composition for producing a foam that exhibits propertiesand performance that are different from that of the base polystyrene. Inthis manner the properties of the final foam product can be customizedto some degree for various intended applications.

DESCRIPTION OF THE DRAWINGS

The features and operation of the invention will be apparent from thefollowing more detailed description of various embodiments of theinvention and as illustrated in the accompanying drawings. Thesedrawings are provided for illustrative purposes only and are not drawnto scale. The spatial relationships and relative sizing of the elementsillustrated in the various embodiments may have been reduced, expandedor rearranged to improve the clarity of the figure with respect to thecorresponding description. The figures, therefore, should not beinterpreted as accurately reflecting the relative sizing or positioningof the corresponding structural elements that could be encompassed bythe example embodiments of the invention.

FIG. 1 is a schematic drawing of an exemplary extrusion apparatus usefulfor practicing methods according to the invention;

FIG. 2 is a schematic drawing of another exemplary extrusion apparatususeful for practicing methods according to the invention;

FIGS. 3A and 3B illustrate a first bending test procedure; and

FIGS. 4A and 4B illustrate a second bending test procedure.

The embodiments detailed below are provided so that this disclosure willbe thorough and complete and will fully convey the scope of theinvention to those skilled in the art. The principles and features ofthis invention may be employed in varied and numerous embodimentswithout departing from the scope of the invention. Indeed, those ofordinary skill in the art will readily appreciate that various of thecomponents illustrated in FIGS. 1 and 2 may be altered or otherwisemodified to provide a range of extruder configurations. As will beappreciated, however, it is primarily the composition of the extrudate,rather than the particular extruder configuration, that provides theunexpected advantages detailed below.

DETAILED DESCRIPTION OF EXAMPLE EMBODIMENTS

Foam boards according to the invention, particularly polystyrene foamboards, are formed by incorporating an amount of one or more vinylresins into the polymeric melt effective to achieve increasedflexibility while substantially maintaining the strength of theresulting foam board products manufactured from polystyrene orpolystyrene blended with other polymers and/or copolymers. Accordingly,rigid extruded polystyrene foam boards manufactured according to theinvention can be easily and repeatedly deformed at ambient temperaturesto produce relative small radii of curvature when compared withcorresponding conventional XPS foam without resiling, cracking orbreaking, and while generally retaining other desirable properties ofconventional foams. This combination of flexibility and strength makesrigid extruded polystyrene foam boards manufactured according to theinvention particularly suitable for producing complex shaped forms.

The rigid, closed cell, polymer foam according to the invention may beprepared using a conventional extruding process with vinyl resinselected from the group consisting of vinyl acetate (EVA),polyvinylalcohol (PVA), vinyl alcohol/ethylene copolymer (EVOH),polyvinylidene chloride (PVDC), polyvinyl chloride (PVC), vinylchloride/vinylidene chloride copolymer, and vinylidenechloride/methylacrylate copolymer, one or more blowing agent and otheradditives and/or PPAs. Without being bound by any particular theory, itis suspected that the benefits, associated with incorporating one ormore vinyl resins in a polystyrene or polystyrene blend resin,particularly the improved deformability of the resulting foams, areattributable, at least in part, to the hydrogen bonding of the vinylresin's hydroxyl group. Consistent with this theory, other polymers andcopolymers including, for example, polyacids and polyamides, containingappropriate hydroxyl or other polar substituents may exhibit similarfunctionality.

A representative vinyl resin is an ethylene vinyl alcohol (EVOH)copolymer resin having ethylene copolymer ratio of about 20 to 40 mol %,more typically about 30 to about 34 mol % (as determined using theKuraray EV-QC-4.17 test method), a melt index of about 1 to 2, moretypically about 1.4 to about 1.8 g/10 min. at 190° C. and about 2.5 toabout 5 g/10 min., and more typically about 3 to about 4 g/10 min. at210° C. (as determined using the ASTM-D1505 test method).

Extruded polystyrene polymer foams of this invention may be prepared inboth twin-screw (low shear), and single screw (high shear) extruders. Atypical extruder comprises multi-feeders containing pellets or beads ofthe selected vinyl resin or combination of vinyl resins that will beincorporated into the polystyrene melt as it is forced through theextruder being added into the extruder along with the basic polymercomposition and any other PPAs or additives through a number of feedinlets. The general procedure utilized in the preparation of extrudedfoam products includes the steps of melting the base polymericcomposition, incorporating one or more blowing agents and otheradditives into the polymeric melt. These compositions are prepared underconditions that are intended to result in the thorough mixing of theblowing agent(s), additives and the base polymer while preventing themixture from foaming prematurely, e.g., by maintaining the blendedcomposition under relative high pressure at least until the mixingprocess has been completed.

This foamable mixture is then typically adjusted to a target dietemperature that may be somewhat below the temperature at which thefoamable mixtures exits the extruder. The foamable mixture is thenextruded through a single or multi-stage extrusion die to reduce thepressure on the foamable mixture to atmospheric or even subatmosphericpressure, allowing the mixture to foam and produce a foamed product. Therapid expansion tends to produce some cooling of the foamed composition,but supplemental cooling, such as immersion baths, may be utilized formore rapid cooling.

As will be appreciated, the relative quantities of the polymer(s),blowing agent(s) and additives, as well as the foaming temperature andthe manner in which the pressure is reduced (e.g., in stages or in asingle step) and the environment into which the polymer is extruded andany subsequent processing will tend to affect one or more of the surfacequality and mechanical properties of the resulting foam product. Afterthe extrusion step, the foam may be subjected to additional processingsteps included, for example dynamic/static cooling, shaping, cutting andpackaging.

As illustrated in FIG. 1, an extrusion apparatus 100 useful forpracticing methods according to the invention may comprise a single ordouble (not shown) screw extruder including a barrel 102 surrounding ascrew 104 on which are provided a spiral flight 106 configured tocompress, and thereby, heat material introduced into the screw extruder.As illustrated in FIG. 1, the basic polymeric composition can be feedinto the screw extruder as a flowable solid, such as beads, granules orpellets, or as a liquid or semiliquid melt, from one or more (not shown)feed hoppers 108.

As the basic polymeric composition advances through the screw extruder,the decreasing spacing of the flight 106, define a successively smallerspace through which the polymer composition is forced by the rotation ofthe screw. This decreasing volume acts to increase the temperature ofthe polymer composition to obtain a polymeric melt (if solid startingmaterial was used) and/or to increase the temperature of the polymericmelt.

As the polymer composition advances through the screw extruder 100, oneor more ports may be provided through the barrel 102 with associatedapparatus 110 that can be configured for injecting EVOH and one or moreadditional polymer processing aids into the polymer composition.Similarly, one or more ports may be provided through the barrel 102 withassociated apparatus 112 for injecting one or more blowing agents intothe polymer composition. Once the polymer processing aid(s) and blowingagent(s) have been introduced into the polymer composition, theresulting mixture is subjected to some additional blending sufficient todistribute each of the additives generally uniformly throughout thepolymer composition to obtain an extrusion composition.

This extrusion composition is then forced through an extrusion die 114and exits the die into a region of reduced pressure (which may be belowatmospheric pressure), thereby allowing the blowing agent to expand andproduce a polymeric foam layer or slab. The polymeric foam may besubjected to additional processing such as calendaring, water immersion,cooling sprays or other operations to control the thickness and otherproperties of the resulting polymeric foam product.

As illustrated in FIG. 2, an extrusion apparatus 200 useful forpracticing methods according to the invention may comprise a single ordouble (not shown) screw extruder including a barrel 202 surrounding ascrew 204 on which are provided a spiral flight 206 configured tocompress, and thereby, heat material introduced into the screw extruder.As illustrated in FIG. 2, the basic polymeric composition, optionallycompounded with an EVOH and one or more additional polymer processingaids, can be feed into the screw extruder as a flowable solid, such asbeads, granules or pellets, or as a liquid or semiliquid melt, from oneor more (not shown) feed hoppers 208.

As the basic polymeric composition advances through the screw extruder,the decreasing spacing of the flight 206, define a successively smallerspace through which the polymer composition is forced by the rotation ofthe screw. This decreasing volume acts to increase the temperature ofthe polymer composition to obtain a polymeric melt (if solid startingmaterial was used) and/or to increase the temperature of the polymericmelt.

As the polymer composition advances through the screw extruder 200, oneor more ports may be provided through the barrel 202 with associatedapparatus 212 configured for injecting one or more blowing agents and,optionally one or more polymer processing aids, into the polymercomposition. Once the desired quantities of polymer, polymer processingaid(s) and blowing agent(s) have been introduced into the screwextruder, the resulting mixture is subjected to some additional blendingsufficient to distribute each of the additives generally uniformlythroughout the polymer composition to obtain an extrusion composition.

This extrusion composition is then forced through an extrusion die 214and exits the die into a region of reduced pressure (which may be belowatmospheric pressure), thereby allowing the blowing agent to expand andproduce a polymeric foam layer or slab. As illustrated in FIG. 2, thispressure reduction may be obtained gradually as the extruded polymericmixture advances through successively larger openings provided in thedie or through some suitable apparatus (not shown) provided downstreamof the extrusion die for controlling to some degree the manner in whichthe pressure applied to the polymeric mixture is reduced. The polymericfoam may also be subjected to additional processing such as calendaring,water immersion, cooling sprays or other operations to control thethickness and other properties of the resulting polymeric foam product.

An XPS foam product according to the invention may be manufactured in afoaming operation having a melt mixing temperature from about 200 toabout 250° C., typically around 240° C., a die melt temperature of about100 to about 130° C., typically around 120° C., and a die pressure ofabout 50 to 80 bar (5 to 8 MPa), typically around 60 bar (6 MPa) whenusing a HCFC 142b blowing agent, with or without incorporating carbondioxide as an additional blowing agent or other blowing aid. Theexpansion ratio, i.e., the ratio of the foam thickness to the extrusiondie gap, may be in the range from about 20 to 70, typically around 60.

A variety of blowing agents may be utilized in forming the foamablemixture including HCFCs, HFCs, CO₂, H₂O, inert gases, hydrocarbons andmixtures thereof. As those skilled in the art with appreciate, althoughcertain blowing agents may be useful in practicing the invention, thereare other considerations, particularly the apparent contribution of CFCcompounds, and perhaps HCFC and HFC compounds as well, to thedegradation of Earth's ozone layer tend to limit their widespread use.Hydrocarbons, for example pentane, hexane and cyclopentane, are moreozone friendly, raise both safety and VOC emission concerns.

Conventional blowing systems may include a composition including one ormore blowing agents, which may also be combined for injection with oneor more PPAs. Such systems include, for example, HCFC-142b comprisingfrom about 8 to about 14%, more typically about 11% of the foamablemixture; HFC-134a comprising from about 4 to about 10%, more typicallyabout 5.5%, in combination with about 3% ethanol; carbon dioxidecomprising from about 3 to about 6%, typically about 3.5 to about 4.0%in combination with about 1.8% ethanol and/or with one or moreadditional PPAs. The PPAs may be used for increasing the solubility ordistribution of the blowing agent throughout the foamable mixture and/orfor altering one or more properties of the completed foam product, forexample the percent of open cells, surface quality and foam density.

The invention was demonstrated by preparing representative examples ofthe inventive rigid polystyrene foam boards and a comparative example ofa conventional rigid polystyrene foam board using both 1) a twin screwLMP extruder in combination with a flat die and shaper plate and 2) asingle screw tandem extruder in combination with a radial die and slinkyshaper. The foam may exit the Vacuum may also be applied in both theabove pilot and manufacturing lines.

TABLE 1 shows the process conditions for examples and control examplewithout EVOH additive in a twin screw extruder. EVOH copolymer isprepared from Eval Company of America's F171 32 mol % EVAL gradematerial. The polystyrene resin used was NOVA 1220 from NOVA ChemicalInc. having a melt index of about 1.6 g/10 minutes. Stabilizedhexabromocyclododecane (Great Lakes Chemical, HBCD SP-75) wasincorporated as a flame retarding agent at a concentration of about 1%by weight of the solid foam polymer. Other additives included about 0.5%by weight talc and trace of colorant. TABLE 1 ControlComponent/Parameter Examples Example Wt. % of EVOH 0.5-2.5 0 Wt. % oftalc 0.5 0.5 Wt. % of CO₂ 3.7 3.7 Wt. % of Ethanol 1.5 1.5 ExtruderPressure, kPa (psi) 13000-17000 (1885-2466) 15800 (2292) Die MeltTemperature, ° C. 117-123 121 Die Pressure, kPa (psi) 5400-6600(783-957) 5600 (812) Line Speed, m/hr (ft/min) 110-170 (6-9.3)    97(5.3) Throughput, kg/hr 100 100 Die Gap, mm 0.6-0.8 0.8 Vacuum kPa (inchHg) 0-54 (0 to 16)  51 (15)

Two inventive and one comparative example of the resulting XPS foamproducts having different EVOH concentrations and physical dimensionsand foam properties as reflected below in TABLE 2 were then subjected tocertain compressive strength and deformation (bending) evaluations.TABLE 2 Control Example 1 Example 2 EVOH Wt %  0 2.5 0.5 Thickness ofBoard - 26.64 (1.049) 25.50 (1.004) 25.17 (0.991) mm (inches) Density(Kg/m³) 29 33 30

The results of the compressive strength and deformation (bending)evaluations are detailed below in TABLE 3. TABLE 3 Control Example 1Example 2 Compressive Strength (kPa) 221 234 214 Bending Tests¹ R_(f) -mm (inches)² 813 (32) 38.1 (1.5) 45.7 (1.8) R_(c) - mm (inches)³ NA 50.8(2)   50.8 (2)   T_(r) ⁴ NA >10 >10¹The test method used in bending tests are detailed below in Paragraphs[0038-43] as applied to samples cut from the sheets with the largerdimension being oriented transverse to the extruding direction.²R_(f) is the radius at failure as further defined below.³R_(c) is the critical radius as further defined below.⁴T_(r) is a measure of the number of times the panel can approach R_(c)without failing.

As can be seen in TABLE 2, the addition of minor portions of EVOH, e.g.,no more than about 2.5% by weight EVOH based on the solid foam polymer,to the foamable polystyrene mixture tended to maintain the compressivestrength while significantly improving the flexibility and thedurability of the of the resulting XPS product. In addition tomaintaining the compressive strength, the example composition foams werecomparable to the control foam with respect to both thermalconductivity, around 0.2 w/m·k thermal conductivity (aged 180 days), andflame retarding, around 15 to 17 seconds burn time for small scaleburning test.

The invention thus provides a high strength-easy deformation (HS-ED)rigid polystyrene foam board which broadens the range of insulationapplications for which XPS insulation may be used, e.g., those thatnecessitate forming different complex shapes, and simplifies theinstallation by reducing or eliminating the need to cut and sealconventional insulating sheets or maintain custom or semicustomconfigurations for complex shapes, thereby reducing construction laborcosts while maintaining or improving the insulating performance of theinstalled product.

The deformation (bending) performance of the inventive foam compositionsand a conventional foam composition as reported above in TABLE 3 wasevaluated using the following procedure(s).

Bending Tests

The Applicants are not aware of a conventional ASTM or ISO equivalentfor this test, but developed this guided bending test for evaluating andquantifying the relative flexibility/ductility of various foam samples.This test is not intended to and does not purport to address all of therigid foam mechanical flexibility properties, such as apparent bendingmodulus (as determined by ASTM D747), or to distinguish between elasticand plastic components. This test does, however, provide a relativelysimple evaluation of an apparent value of the allowed bending radius aswell as a measure of the durability of the foam board by bending thefoam board up to ten times (or to failure if the board is notsufficiently durable to endure the repeated deformations).

Other tests that could be used for evaluating the performance of XPSfoam products include bending tests addressing various types of bendsincluding free bending, guided bending (for example, ASTM E190),semi-guided bending (for example, ASTM E290), and wrap around bending.Other tests include cantilevered beam bending modulus (for example, ASTMD747) which determine the apparent bending modulus by measuring forceand angle of bend of a cantilever beam.

The tests were conducted on rectangular test samples cut from the XPSsheets measuring 4 inches×24 inches (10×61 cm). The thickness of testsamples reflected the thickness of the product sheets being tested.These test samples were then subjected to the two different bendingtests.

As illustrated in FIGS. 3A and 3B, Test A was a semi-guided bendingtest, in which the test samples were placed above the bending guidefixture FIG. 3A (the guide fixture being a steel tube having a diameterselectable from 2 inches to 6 inches (5 cm to 15 cm)) and sufficientforce was applied to hold down both sides of the sample. As the samplewas being deformed, the central convex region C of the sample was thenexamined for cracking or other strain-induced defects that wouldindicate sample failure. The deflection or midordinate, Δ, at failurewas recorded for each sample. The radius at failure, R_(f), was thencalculated according to formula I:R _(f)=(L ²/8Δ)+Δ/2  (I)in which L=chord length for measuring deflection (24 inches for thesesamples) and Δ=the deflection or midordinate, in inches.

As illustrated in FIGS. 4A and 4B, Test B was a parallel-on-itself 180°bending test, in which the test procedures are as follows by using thesame bending guide fixture utilized in the Test A procedure. The sampleswere placed above the bending guided fixture and sufficient force F wasapplied to bring the opposite sides of the sample into a parallelorientation, FIG. 4A, the separation between the parallel sides, andconsequently the radius of the arcuate portion of the sample, wasreduced until the sample failed, e.g., cracked in the central convexregion. This radius was recorded as the critical radius, R_(c).

As illustrated in FIG. 4B, the samples were then repeated bent to nearthis critical radius first in a primary direction and then in thereverse direction (indicated in dashed lines) until cracking wasobserved occurred on central convex surface of the sample or until 10bending cycles had been completed. The number of cycles endured by thesample, T_(r), was recorded at failure or upon termination of the test,i.e., T_(r)>10.

Although non-limiting example embodiments of the invention have beendescribed in detail above, it should be understood that many variationsand/or modifications of the basic inventive concepts taught herein,which may be readily apparent to those skilled in the art, will stillfall within the spirit and scope of the example embodiments of theinvention and as defined in the appended claims.

1. A method for producing expanded polystyrene foam products comprising:preparing a pressurized foamable composition including a major portionof polystyrene, a first minor portion of bending agent and a secondminor portion of blowing agent; extruding the pressurized foamablecomposition through a die into a region of lower pressure to form anintermediate foam product; and cooling and finishing the intermediatefoam product to form a final foam product.
 2. The method for producingexpanded polystyrene foam products according to claim 1, wherein: thebending agent is selected from at least one of vinyl acetate (EVA),polyvinylalcohol (PVA), vinyl alcohol/ethylene copolymer (EVOH),polyvinylidene chloride (PVDC), polyvinyl chloride (PVC), vinylchloride/vinylidene chloride copolymer, and vinylidenechloride/methylacrylate copolymer.
 3. The method for producing expandedpolystyrene foam products according to claim 1, wherein: the bendingagent is a vinyl alcohol/ethylene copolymer (EVOH).
 4. The method forproducing expanded polystyrene foam products according to claim 1,wherein: the bending agent is a vinyl alcohol/ethylene copolymer (EVOH)having a melt index from about 1.5 to about 1.8 at about 190° C.
 5. Themethod for producing expanded polystyrene foam products according toclaim 1, wherein: the bending agent is a vinyl alcohol/ethylenecopolymer (EVOH) having a melt index from about 1.5 to about 1.8 atabout 190° C. and an ethylene composition from about 30 to about 34 mol%.
 6. The method for producing expanded polystyrene foam productsaccording to claim 1, wherein: the bending agent is a vinylalcohol/ethylene copolymer (EVOH) that represents less than about 5 wt.% of the foamable composition based on a dry weight of the foamedproduct.
 7. The method for producing expanded polystyrene foam productsaccording to claim 1, wherein: the bending agent is a vinylalcohol/ethylene copolymer (EVOH) that represents no more than about 2.5wt. % of the foamable composition based on a dry weight of the foamedproduct.
 8. The method for producing expanded polystyrene foam productsaccording to claim 1, wherein: the bending agent is a vinylalcohol/ethylene copolymers (EVOH) that represents no more than about0.5 wt. % of the foamable composition based on a dry weight of thefoamed product.
 9. The method for producing expanded polystyrene foamproducts according to claim 1, wherein: the pressurized foamablecomposition also includes a minor portion of an olefinic polymer orolefinic copolymer other than polystyrene.
 10. The method for producingexpanded polystyrene foam products according to claim 1, wherein: thebending agent incorporates a plurality of polar groups that will tend toform hydrogen bonds with the polystyrene.
 11. The method for producingexpanded polystyrene foam products according to claim 10, wherein: amajority of the polar groups are hydroxyl groups.
 12. A rigid expandedpolystyrene foam product comprising: a major portion of polystyrene; afirst minor portion of a bending agent; and a second minor portion of ablowing agent, wherein a transverse sample having a nominal thickness ofabout 1 inch (about 2.54 cm) has a radius at failure R_(f) of less thanabout 12 inches.
 13. The rigid expanded polystyrene foam productaccording to claim 12, further including: a third minor portion of oneor more polymers and copolymers compatible with the major portion ofpolystyrene, and wherein the first minor portion of the bending agent isa blend of at least two bending agents, and further wherein the secondminor portion of the blowing agent is a blend of at least two blowingagents.
 14. The rigid expanded polystyrene foam product according toclaim 12, wherein: the first minor portion of bending agent including atleast one compound selected from at least one of vinyl acetate (EVA),polyvinylalcohol (PVA), vinyl alcohol/ethylene copolymer (EVOH),polyvinylidene chloride (PVDC), polyvinyl chloride (PVC), vinylchloride/vinylidene chloride copolymer, and vinylidenechloride/methylacrylate copolymer; and the second minor portion ofblowing agent including at least one compound selected from at least oneof HCFCs, HFCs, CO₂, H₂O, inert gases, hydrocarbons and mixturesthereof, and wherein a transverse sample having a nominal thickness ofabout 1 inch (about 2.54 cm) has a radius a Test A failure radius R_(f)of less than about 12 inches.
 15. The rigid expanded polystyrene foamproduct according to claim 12, wherein: the bending agent is a vinylalcohol/ethylene copolymer (EVOH).
 16. The rigid expanded polystyrenefoam product according to claim 12, wherein: the bending agent is avinyl alcohol/ethylene copolymer (EVOH) having a melt index from about1.5 to about 1.8 at about 190° C.
 17. The rigid expanded polystyrenefoam product according to claim 12, wherein: the bending agent is avinyl alcohol/ethylene copolymer (EVOH) having a melt index from about1.5 to about 1.8 at about 190° C. and an ethylene composition from 30 to34 mol %.
 18. The rigid expanded polystyrene foam product according toclaim 12, wherein: the bending agent is a vinyl alcohol/ethylenecopolymer (EVOH) that represents no more than about 2.5 wt. % of thefoamable composition based on a dry weight of the foamed product. 19.The rigid expanded polystyrene foam product according to claim 12,wherein: the bending agent is a vinyl alcohol/ethylene copolymer (EVOH)that represents no more than about 1.0 wt. % of the foamable compositionbased on a dry weight of the foamed product.
 20. The rigid expandedpolystyrene foam product according to claim 14, wherein: the bendingagent is a vinyl alcohol/ethylene copolymer (EVOH) that represents nomore than about 2.5 wt. % of the foamable composition based on a dryweight of the foamed product and wherein a transverse sample having anominal thickness of about 1 inch (about 2.54 cm) has an R_(f) of lessthan about 6 inches.
 21. The rigid expanded polystyrene foam productaccording to claim 14, wherein: the bending agent is a vinylalcohol/ethylene copolymer (EVOH) that represents no more than about 2.5wt. % of the foamable composition based on a dry weight of the foamedproduct and wherein a transverse sample having a nominal thickness ofabout 1 inch (about 2.54 cm) has an R_(f) of less than about 4 inches.22. The rigid expanded polystyrene foam product according to claim 14,wherein: the bending agent is a vinyl alcohol/ethylene copolymer (EVOH)that represents no more than about 2.5 wt. % of the foamable compositionbased on a dry weight of the foamed product and wherein a transversesample having a nominal thickness of about 1 inch (about 2.54 cm) has anR_(f) of less than about 4 inches and a critical radius R_(c) of lessthan about 12 inches (about 30.5 cm) measured according to Testprocedure A.
 23. The rigid expanded polystyrene foam product accordingto 19, wherein: the polystyrene foam product having a nominal thicknessof about 1 inch (about 2.54 cm) has an R_(f) of less than about 4 inchesand a critical radius R_(c) of less than about 6 inches (about 15.2 cm)measured according to Test procedure B.